Flexible rubber articles reinforced with fiber of certain polyamide-hydrazide polymers

ABSTRACT

FLEXIBLE RUBBER ARTICLES REINFORCED WITH HIGH TEMPERATURE ORGANIC FIBERS HAVING DENSITIES GREATER THAN 1.37 G./ ML. AND UNUSUALLY HIGH INITIAL MODULI OF OVER 700 GRAMS PER DENIER AT ELONGATIONS OF 2% OR GREATER ARE DISCLOSED. THE REINFORCING FIBER ELEMENTS ARE MADE FROM WHOLLY AROMATIC POLYMERS HAVING MELTING POINTS ABOVE 200*C. AND INHERENT VISCOSITIES OF AT LEAST 3.5 THE POLYMERS ARE FURTHER CHARACTERIZED IN THAT THE RECURRING DIVALENT AROMATIC RADICALS ALONG THE POLYMER CHAIN ARE AT LEAST ABOUT 85 WEIGHT PERCENT PARA-ORIENTED, HAVE A PLANE OF SYMMETRY OR ARE LINKED BY RING ATOMS REPRESENTING THE MAXIMUM SPACING. THE FIBERS ARE PARTICULARLY USEFUL AS REINFORCING ELEMENTS IN V-BELTS, CONVEYOR BELTS AND PNEUMATIC RUBBER TIRES, AND ESPECIALLY IN THE BELT PLIES OF BELTED TIRES.   D R A W I N G

BRIAN K. DANIELS JACK PRESTON DAVID A. ZAUKELIES INVENTORS BY 5 ATTORNEY IO H l2 l3 I4 l5 INITIAL MODULUS GRAMS DENIER B. K. DANIELS ETAL Filed June 30, 1971 POLYAMIDE'HYDRAZ IDE POLYMERS Feb. 20, 1973 FLEXIBLE RUBBER ARTICLES REINFORCED WITH FIBER OF CERTAIN O O O O O O O O Q O O O 7 6 5 4 3 2 SINGLE FILAMENT ELONGATION TO BREAK E Patented Feb. 20, 1973 3 17 a tire belt reinforced with an organic fiber having a high 9 tenacity, low elongation and a high modulus.

Another object of the invention is to provide other POLYMERS rubber articles, such as, V-belts, conveyor belts, rubber Brian K. Daniels and Jack Preston, Raleigh, NC, and 5 hoses and the like, reinforced with an organic fiber hav- David A. Zaukelies, Pensacola, Fla, assignors to Mong a gh tenacity, low elongation and a high modulus. santo Company, St. Louis, Mo.

Continuation-impart of application Ser. No. 748,55?, July SUMMARY OF THE In 'ENTION i :3 3 g lg slatgrqit $300,269. This app icatio The present invention provides rubber articles reinlme 4 10 forced with fiber of an organic polymer, wherein the The P 3 g glifii g' fiza to fiber has a specific density of at least 1.37, single filament i 5 6 5 /02 27/34 elongation-to-break (E ranging from 2.0 to 15 percent Us. Cl. 6 11 Claims and an initial modulus in grams per denier greater than the value, 1000 (E and wherein said polymer has 15 a melting point above 200 C. and a structure repre- ABSTRACT OF THE DISCLOSURE sented by the following formula Flexible rubber articles reinforced with high tempera- 6'' ml. and unusually high initial moduli of over 700 grams 20 .121

per denier at elongations of 2% or greater are disclosed. whereln Ar and Ar represent aromatic carbocyclic resi- The reinforcing fiber elements are made from wholly dues, aromatic heterocyclic residues and combinations aromatic polymers having melting points above 200 C. thereof which must be at least about 85 weight percent and inherent viscosities of at least 3.5. The polymers are para-oriented, have a plane of symmetry or are linked further characterized in that the recurring divalent aroby ring atoms representing the maximum spacing, any matic radicals along the polymer chain are at least about extracycllc bonding within said aromatic residues being 85 weight percent para-oriented, have a plane of symthrough a radical selected from the group consisting of metry or are linked by ring atoms representing the maxi- S mum spacing. The fibers are particularly useful as reinll ll NH forcing elements in V-belts, conveyor belts and pneumatic rubber tires, and especially in the belt plies of and Combmatlons thereof; and R" are radicals sebelted tires. lected from the group consisting of This application is a continuation-in-part of applicaand combinations thereof, y and y are the values 0 or 1 1;?51 748,559, filed July 29, 1968, H and n is a number large enough to provide a polymer having an inherent viscosity of at least 3.5. BACKGROUND F THE INVENTION Particularly preferred fibers for use in the invention It is known to reinforce flexible rubber articles, such as are those composed of a polymer having recurring units pneumatic tires, with cords or strands of organic or inorof the structure 0 o o 0 II ll 0 0 II ll ganic material. Cotton, rayon, nylon and polyester have DETAILED DESCRIPTION OF THE INVENTION been used as basic tire cords in tire carcasses, while primarily fiber glass and steel wire have been used in tire igz gj t igzi gvltlerem s i filament belts. Recently, there has been a widespread and growing 60 t th 1 h 168 e ween an 15 pe.rcent interest in belted tires in the United States As a result Cons I u es 1 e S ope 9 t 6 curve AB on the graph m the figure. Thus, the family of fibers em 10 ed in th t t there is a need to develop an orgamc fiber that is competip 6 ms an tive with fiber glass and steel wire for the reinforcement of i T 112088688 mmal moquh of greater than tire belts. Organic fibers ofier certain advantages over 3 g; f g f g g and an steel wire, for example, they are lighter weight and are 1 T 0 g ea er an a out at 2 .percent easier to process and handle. In general a belt cord must e-ongatlon' hese ej-itraorduiary propFmes are umque f have the following properties. g dynamic modulus high temperatufre, high density orgamc fibers and provide a versa 1 ity 0 property relationships within the abovehigh stiffness, high strength, low growth and creep (diindicated B hi mensional stability), high compression modulus and at proached gj g i g not heretofore been apleast minimal fatigue requirements.

The class of polymers capable of being spun into the A speclfic ob ect of the present mvention 18 to provlde high modulus fibers used in this invention are wholly aromatic linear polymers which provide rigid chains such that the ability for the polymer chain to fold, rotate in random coil or irregular fashion is minimized. That is, it is essential that there must be little irregular molecular spin along the chain so that the oriented molecules in the fiber form are capable of packing to the extent that fiber densities of 1.37 or greater can be achieved. Etficient or close molecular packing, reflected by the fiber density is essential to the achievement of the greatly superior and unique combination of properties possessed by the fibers of this invention. To insure rigidity along the polymer chain, the recurring divalent aromatic radical along the polymer chain must have centers of symmetry, as in the case of 1,5-naphthylene, 2,6-naphthylene, and 4,4-biphenylene, or simply be all para oriented, or they may be a combination of para oriented aromatic radicals along with other aromatic radicals having centers of symmetry. Another essential feature of this class of polymers is that the recurring aromatic radicals along the polymer chain must be linked in the chain through carbocyclic carbon atoms to one of radicals. These interlinking groups and combinations of them, such as to the exclusion of those radicals which allow the polymer chains to fold, bend or otherwise penetrate the circumference of the theoretical cylinder formed by the orbital molecular rotation of molecules in a rigid chain polymer, are essential to the achievement of superior fiber properties. We have also found that the above-described aromatic radicals may be linked in the polymer chain, without disruption of chain rigidity, by single or multiple ring aromatic heterocyclic radicals which do not allow the chain to bend or told as reflected by fibers prepared therefrom having densities greater than 1.37.

The aromatic heterocyclic radicals which may be present in the wholly aromatic polymers are unsubstituted and 6 membered rings containing only the C, O, S and N. In order to maintain the chain rigidity necessary for this invention the heterocyclic radicals must contain at least two extracyclic interlinear covalent bonds which are non-adjacent with respect to the cyclic atoms of the ring. Additionally, at least two extracyclic interlinear covalent bonds must be oriented with respect to one another at maximum spacing. These requirements apply with respect to the single rings in the case of a multi-ring system. Exemplary of such ring systems are the following radicals:

Thus, the key to the orientation of the carbocyclic or heterocyclic radicals which may form links in the polymer chains is that the covalent bond at one end of a given radical must be that which is the greatest distance possible from the other bond or bonds linking the radical in the polymer chains.

In addition to the chemical requirements for the polymers above-mentioned there are two other physical properties of the polymer which must be observed before fibers spun from the polymers can achieve the remarkable properties of the fibers disclosed. The polymer must not melt at temperatures below about 200 C. which provides good fiber properties in many use application without which other fibers having similar properties would not be useful.

In this respect polymers employed in the fiber reinforcing elements of this invention exhibit only slight changes in dynamic mechanical modulus (less than about 20 percent in Vibron determinations run at 11 cycles/ second) in the range from 25 C. to 200 C. indicating excellent retention of properties over a wide temperature range. This characteristic differs greatly from that found in many other polymers and permits use of the fibers of the invention as composite reinforcements with a variety of fabrication techniques in which other organic reinforcing fibers Wuold be degraded to the extent that their utility as reinforcing materiais would be essentially negated.

Moreover, the polymers used to make the fibers used in this invention must have molecular weights high enough to reflect inherent viscosities of at least 3.5. It has been generally observed that polymers of the class mentioned above, even though corresponding to other essential requirements, do not provide fibers having the properties of the fibers used in this invention unless the inherent viscosities are greater than 3.5.

Even though the viscosities of the polymers necessarily employed in this invention are unusually high for forma-' tion of fibers, the average molecular weights of the rigidchain polymers necessary to achieve such viscosities are quite low when compared to molecular weights of fiber forming polymers of the well-known acrylic, polyolefin and alphatic polyamide types. Thus, the number average molecular weights of the high viscosity polymers used in this invention may lie in the range of 50,000 to 100,000, for example, whereas fiber-forming polyolefins characteristically possess molecular Weights of much higher order.

As long as the linearity, the rigidity, the viscosity, the stability to heat up to 200 C. and chemical nature of the polymers are observed in accordance with the limitations described, the method of polymer preparation has not been found'to be critical. Accordingly, the polymers may be prepared by any convenient means. Perhaps the most convenient means comprises solution polymerization of appropriate aromatic diisocyanates or diacide halides with essentially equimolar quantities of difunctional wholly aromatic monomers containing ter minal --NH radicals.

These reactions may conveniently be illustrated as follows:

to the extent that the arrangement of repeating or alternating units may be such that the polymers range from wherein Ar and Ar may be the same or different wholly aromatic, single or multiple ring, carbocyclic or heterocyclic residues and combinations thereof, R and R" may be the same or different divalent groups,

A representative polymer system which may be ern ployed to illustrate the polymer, its preparation and spin- L ning to form the novel and superior organic fibers used in this invention is an essentially linear wholly aromatic polyamide-hydrazide polymer which contains the alternating units characterized by the following formulas:

II II -C--Ar--O (I) and O NH-Ar( NHNH (II) wherein Ar and Ar represent the same or different divalent aromatic residues which must be a para oriented single ring, or a multiple or fused ring system containing a center of symmetry with respect to the extracyclic covalent bonding sites, or in the case of aromatic hetero cyclic rings the extracyclic bonding must be such that the interlinear spacing is at a maximum distance. Such radicals, in addition to those already mentioned, include the following:

wherein R may be radicals such as and others hereinabove described, and combinations thereof.

Thus, the wholly aromatic polyamide hydrazide may be represented by repeating segments having the formula:

{hat s wherein Ar and Ar are above defined. The parentheses in Formula IH connote the fact that the alternating units, I and H, may occur in head-to-head or head-to-tail fashion (III) wholly ordered polymers to polymers having no discernible order as is hereinafter described in greater detail.

In general the wholly aromatic polyamide hydrazides above-described may be prepared through polymerization reactions involving one or two steps. In the case of a two-step reaction, the first step involves the preparation of an amine terminated aromatic dihydrazide, repre sented by IV. The second step involves reaction of IV:

0 O A r( JNHNH( /ArNH:

with equimolar quantities of aromatic diacid halide. The product of a two-step reaction is an essentialy wholly ordered polymer of regularly recurring segments which segments are represented by the following formula:

The term, essentially wholly ordered, as employed herein is intended to connote the orderly arrangement of molecules precisely as set forth in the repeating segment of Formula V and is intended to include those specific compositions which are characterized by such arrangement of molecules, even though an occassional Ar or Ar group may be derived through the use of a mixture of essentially functionally equivalent monomers.

The one-step preparation of the wholly aromatic polyamidehydrazide may be achieved through the reaction of essentially equimolar quantities of an aromatic diacid halide and an aromatic amino-hydrazide as depicted using p-aminobenzhydrazide and terephthaloyl chloride in the following reaction scheme:

Insofar as chemically unsymmetrical monomers such as p-aminobenzhydrazide can enter the polymer in either head-to-head or head-to-tail fashion, as mentioned earlier, no single repeat segment (represented by Formula V) is assured as in the case of the above-described two-stage reaction. Therefore, when referring to the arrangement of units of Formula II the parentheses employed, as in Formulas II and III and reaction VI indicate that such units may occur in reverse order with respect to any such unit along the polymer chain. Thus, the polymers used to prepare the fibers employed in this invention may comprise one or more units having the formulas:

(VII) and used in the sense of being polymer chain segments and particles in the dopes, particularly in dopes of high not necessarily repeating segments or units so that as viscosities, the addition of small amounts of water serves either x or y approaches in Formula X: to improve dope stability. Spinnability of the high visthe polymer becomes a more ordered polymer (x and y yh p f q y the iflventien eel! be improved are average numbers, including zero [the sum of x and y] y mild heatlng to reduce vlseoelty- The P y dOPeS being representative of the average sequence lengths of are P y, but not critically, held at temperatures segments VII and VIII, respectively). As a general rule, between about and p h y from it has been found that those reaction conditions which Q and and at P y e11ee11trat1n5 of from increase the degree to which the reaction is kinetically about 4 to 12 Percent y Weight of Solids, heth patafneters controlled will result in an increase in the order of the 15 depending Primarily 0n the average meleetltal' welght of polymer produced, whereas, those conditions which inthe P y as reflected y its inherent tY- e crease the degree to which the reaction is diffusion con- Over, in 'yl Wet Spinning Operations the Optlmum trolled will result in decrease in the order of the polymer tanee 0f the l face from the Surface of the eoegutatlon produced. bath generally lies within the range of from about one- The above-described polyamide hydrazide polymers eighth to about one-half of an dependmg 011 may be prepared through the use of known solution and COSitY, temperature and other eenthtlonsinterfacial techniques. However, since neither the inter- The versatility of fibers 0f t class of Wholly t mediate dihydrazide diamine of Formula IV nor the final Ihetie P y desertbed herein can be reahzed P polymer of either the one-step or two-step preparation p y thfeugh vafletlofl of P y ehemleel eneed be isolated prior to polymerization or prior to the tlon, Viseesltl and Splnmng eondltlonee aehleve maxi formation of fibers according to this invention, the solumum tensile Properties, P y having high e p tion polymerization technique is highly preferred. PEtra Orientation Should be employed et h PQ Y' Solution polymerization generally involves the dissolu- Viscosittee and Spun under eQIldltlOhS which 1111111- tion of the dihydrazide diamine of Formula IV or the mile the p ot'ientetiotl y minimizing the Stretch aromatic amino-hydrazide monomers in a suitable solvent ing the eoagulatltm and m a hot Water cascade and therewhich solvent is also a solvent for the aromatic diacid after thermally Stretching h fiber f generally halide and the product polymer. Typical of such solvents non'eqtteolls eehthtlene t0 lmpttft maximum Stretch are N,Ndimethylacetamide, N-methyl 2 pyrrolidone, Orientation h erystalhmtyhexamethylphosphoramide and mixtures of these and like More Pattlcularly, Where fibers hevlng modulus Values solvents. In many instances, such solvents are rendered exceeding those of t best glass fibers are e the more effective by mixing them with small quantities, gen- P deserlbed Formula} HI Should be hlghly P erauy not more than about ten percent by Weight, f a oriented, thus the divalent residue Ar should be greater salt of an alkali or alkaline earth metal, such as lithium than 85 Weight p h P Oriented sheuld be chloride, calcium chloride, magnesium bromide and the 40 t greatBr h Welght Perce'nt f oneflted W1th any like. Preferred among such solvents for the polymerizadlfierent onefltatlon the YeSIfIue bemg Fssemlany [ion is N,N dimethy1acetamide (DMAC), and Especially meta orientat on. Quasi-para orientation occurs in the case DMAc containing a small amount of dissolved lithium of hetemcychc mugs Such chloride. To the solution of the dihydrazide diamine or aromatic amino-hydrazide reactant maintained at a temperature between 30 'C. and 100 0., preferably between -20 C. and 35 C., the aromatic diacid halide is added as a solid, at liquid or as a solution. The reaction \0 mixture should be stirred during addition of the aromatic diacid halide and until the reaction is substantially comwhere the orientation represents considerably greater plete or until the desired viscosity is obtained. Hydrogen maximum spacing than meta orientation and slightly less halide by-product should be neutralized upon completion than para orientation at maximum possible distance for of the polymerization reaction in order to reduce its corthe particular radical. Therefore, in the consideration of rosive eifects or extrusion or other handling equipment. chain rigidity of the polymers employed in the instant This may be accomplished by adding essentially stoichioinvention it will be observed that radicals possessing metric quantities of materials such as lithium hydroxide, quasi-para orientation can occur considerably more frelithium carbonate, calcium carbonate, calcium acetate and quently along the polymer chain than in the case of the like. meta-oriented radicals without sacrifice of chain rigidity.

Superior fiber reinforcing elements of this invention It has been found that the X-ray ditfractions of high have been prepared employing wet spinning or a dry-jet modulus fibers of polymers made from terephthaloyl wet spinning technique, the latter technique being where chloride and p-aminobenzhydrazide are collagen-like the solution of polymer is extruded from one or more with respect to the numerous orders of reflection in the orifices situated a short distance above the surface of a longitudinal direction, indicating a high degree of regucoagulation bath, into a gaseous atmosphere and then into larity over long distances in the polymer chain. This is the coagulation bath principaly composed of Water and a interpreted to mean that the polymer is not chainfolded minor proportion of the solvent or solvents employed in but in the extended configuration. Such an interpretation the spinning solution to thereby coagulate the freshly is also consistent with electron diffraction data obtained extruded filament in gel form. The gel filament, resulting on these polymers and their almost total lack of any from either wet spinning or dry-jet wet spinning is therelow angle X-ray scattering. The high moduli of the fibers after washed to extract salts and solvent, wet-stretched, of the instant invention difier from fibers made from dried, optionally given a conventional textile antistatic polymer whi h contain tetrahedral carbon atoms, metaand/or lubricant finish, optionally heat-stretched and phenylenes, cyclohexane and similar ring structures, all packaged. Spinnability of the aromatic polymers is exof which contain chainfolding or a zig-zag array of cellent so long as the dopes remain gel-free. Where there chain units. Insofar as the fibers of this invention are is a tendency toward gross gellation or to form gelled in the fully extended state or nearly so, stress is to a large extent against the para-phenylene rings which can yield little under stress thus:

While the polymers useful in making the fibers used in this invention have been illustrated in great detail with respect to a given system for purposes of being concise, other polymers, for further example, represented by the formulas:

prepared by polycondensation of terephthaloyl halide with appropriate amines, can also be used to make the fibers described herein by spinning processes which result in high stretch orientation to result in fibers having densities greater than 1.37 as earlier indicated.

Inherent viscosities of fiber described herein can be determined in any suitable polymer solvent such as N- methylpyrrolidone, dimethylacetamide, dimethylacetamide with lithium chloride, concentrated sulfuric acid, dimethylsulfoxide, hexamethylphosphoramide and the like generally as 0.5 percent solution of polymer at about 30 C. Similarly, viscosities can be determined at other concentrations where convenient, for example, 0.1 percent solutions can be employed.

Fiber densities as herein described are readily obtained by placing a fiber sample in a liquid having a density lower than that of the fiber sample and raising the density of the liquid by addition of another liquid having a density greater than that of the fiber sample until a liquid/fiber density equilibrium is achieved after which the density of the equilibrium density liquid can be accurately measured on a Fisher-Davidson Gravitometer. The term density used herein is intended to be synonomous with specific gravity.

Birefringence values reported herein were obtained using an Ehringhaus High Order Compensator.

The present invention is further illustrated by the followering examples which are not intended to be limiting in any respect. In the examples, the fiber, tenacity, elongation and modulus values were obtained using an Instron Tester (Model No. TM) with a l-inch gauge length and an extension rate of 100 percent per minute. The fiber samples were preconditioned at 65 percent relative humidity at 70 F. for 24 hours prior to testing, and then tested at these conditions. The data presented are generally the result of 5 breaks.

In the following examples, the preparation of all polymers was carried out under nitrogen. The polymer solutions were spun into a water bath at 20 0., containing 0-2 percent dimethylacetamide, unless stated otherwise. Spinning speeds were generally about 100' per minute. Hot-drawing was carried out over a 12" hot block with profile temperature.

The organic fibers described herein may be used in a conventional manner to provide reinforced flexible rubber articles.

EXAMPLE I A clean, dry 30-gallon Pfaudler reactor equipped with stirrer, gas inlet tube and drying tube was purged with nitrogen and charged with 139 lbs. (66.725 liters) of dry DMAc. A 0.24% excess of para-aminobenzhydrizide (PABH), 2727.8 grams, was then added to the reactor and dissolved in the DMAc. The reactor temperature was adjusted to between and l5 C. at which temperature 3654.5 grams of solid terephthaloyl chloride (TCl) was added to the solution with rapid stirring. Up-

ture reached a temperature of 50 C. The reaction mixture was then degassed by vacuum for one hour. A polymer solution containing 6.7 solids was obtained having a Brookfield viscosity at 25 C. of 9,250 poises and an inherent viscosity of 6.49 (0.1 gram in 100 ml. of dimethylsulfoxide [DMSO] at 30 C.).

The dope, thus prepared, was pumped at a rate of 40.5 cc./min. into an aqueous coagulation bath maintained at 20 C. from a 7 mil., -hole spinnerette situated a small distance above the surface of the bath with a calculated jet-stretch of 1.0x, washed in an aqueous cascade bath with a calculated cascade stretch of 1.33 X, dried first at C. and then at C. on rolls and then subjected to a two stage hot stretch of 1.25 and 1.10 at temperatures of 300 C. and 350 C., respectively. The fiber thereafter was collected on a bobbin. The processed fiber EXAMPLE II A polyamide-hydrazide polymer solution was prepared and spun into fiber according to the procedure described in Example I. Tire cord was made from the fiber, the cord construction being 1050/3 cord 6 x 4.5 twist, where the 6 and 4.5 are twists in opposite direction. The cord had the following properties:

Denier *3332 Tenacity g.p.d 7.12 Elongation percent 10.9 Growth 0.6

Strength: approx. 5 lbs.

EXAMPLE III The following G-78 x 14 tubeless tires of belted bias construction were built using the following indicated cord in the plies:

Body plies Belt plies (18 ends per inch) Tire N o.

2, Nylon 66 2, Example II cord 1-2 Do..." 2, ass 3-4 2, polyester 2, Example II cord 5-6 Do 2, glass 7-8 The tires were mounted on automobiles and inflated to 24 p.s.i.g. and supported a 1380 lb. standard load. The automobiles were driven on a 9 mile circumference test track in Texas at 70 mph. for 19,000 miles. Each of the tires were then examined for tire performance and tread wear. The results of the test are given in Tables 1 and 2.

TABLE 1.TIRE PERFORMANCE Tire No Construction Mileage Failure Nylon 66, Example II eord 19,000 None.

do 19,000 Do. Nylon 66, glass 19,000 Do. do 19,000 Do. Polyester, Example II cord 19, 000 Do. 6 -do 7, 625 Separation-belt edge. 7 Polyester, glass- 19, 000 None. 8 -do 400 Separation ofl belt.

TABLE 2.TREAD LOSS (MILES/MIL) AT 19,000 MILES The data in the above tables show that rubber tires reinforced with the fiber of Example II provlde good performance and tread wear.

EXAMPLE IV This example illustrates another polyamide-hydrazide fiber which may be used to reinforce rubber articles.

4.32 g. (0.01 m.) of the diamine,

through a spinnerette having an array of 90, 7 mil. diameter orifices into air for a short distance and into an aqueous coagulation bath containing a minor proportion of DMAc. The coagulated filaments were continuously passed from the coagulation bath into a water cascade at 65 C- and thereafter dried on a first godet at 100 C. and a second godet at 150 C. The dried filaments were then heat stretched by passing them over a first shoe at 300 C. and a second hot shoe at 350 C. and thereafter taken-up. The stretching involved in the spinning process consisted of a 1.0x jet stretch during coagulation, 1.4x cascade stretch, 1.3x stretch on the first hot shoe and a 1.04X stretch on the second hot shoe. The collected fiber was characterized and exhibited the following properties:

Denier--6.26

Tenacity14.3 grams/denier Elongation )3.7

Modulus594 grams/ denier Work-to-break (g./cm./den./cm.).33

The following results indicate the wide variety of properties obtainable from a given polymer solution, as a result of minor variations in the spinning conditions used.

Work to Elonbreak Tenacity gation Modulus (g. lem. I

Sample (g.p.d.) (percent) (g.p.d.) d./em.)

o o o o H 1% H M NH!" CNHNH CNHNHC- NH:

prepared from an excess of p-aminobenzhydrazide and terephthaloyl chloride, was dissolved in 70 ml. of DMAC containing 5 percent dissolved lithium chloride under nitrogen. The solution was cooled to 10 C. and 2.03 g- (0.01 m.) of terephthaloyl chloride was added. After 10 minutes, the clear viscous polymer solution which formed was warmed to room temperature, and an additional 20 ml. of DMAc with 5 percent dissolved LiCl Was added. After stirring for 30 minutes at room temperature the dope was neutralized by the addition of 0.67 g. (90 percent of theory) Li CO and 10 ml. DMAc. The 5 percent polymer dope was stirred at room temperature for 1 hour, at 50 C. for 30 min. and then at 80 C. for 20 min. The dope was then degassed under house vacuum for 10 minutes. The polymer had an inherent viscosity of 5.08 (0.5 percent in DMSO at 30 C.).

The polymer solution having a Brookfield viscosity of 24,000 poises was spun through a 5 mil., 10 hole jet, at a jet-stretch of 2.34, a cascade stretch of 1.14 and a dried temperature of 150 C. One sample of fiber (a) was hotdrawn 1.25 X at 300 C., while a second sample (1)) was not hot-drawn. Unaveraged single filament properties of these fiber samples are given in the following table.

A polyamide-hydrazide prepared in the manner decribed in Example I was dissolved in DMAc to provide a dope containing about 6 weight percent of polymer solids and having a Brookfield viscosity of 9,000 poises. The dope at 45 C. was pumped at a rate of 40.5 cc./min.

0 H;NH-(R') -Ar-(R"), -NH-ii-Ar'ii] wherein Ar and Ar represent aromatic carbocyclic residues, aromatic heterocyclic residues and combinations thereof which must be at least about percent para-oriented, have a plane of symmetry or be linked by ring atoms representing the maximum spacing, any extracyclic bonding within said aromatic residues being through a radical selected from the group consisting of 0 s -o-, -ii-, NH-, N=N- and combinations thereof, R' and R" are radicals selected from the group consisting of AL, AL, NH

and combinations thereof, y and y are the values 0 or 1 and n is a number large enough to provide a polymer having an inherent viscosity of at least 3.5.

2. The article of claim 1 wherein the fiber is embedded in the rubber as a continuous filament.

3. The article of claim 1 wherein the fiber is embedded in the rubber in the form of a fabric.

4. The article of claim 1 wherein Ar and Ar are phenylene radicals.

14 5. The article of claim 4 wherein Ar and Ar are para- 10. The article of claim 7 wherein the fiber is comphenylene radicals. posed of polymer represented by the formula 0 o 0 Y Q" Q "Q HNH- G-NH NH-C NH-C -o OH I- In 6. The article of claim 1 wherein R" is wherein n is a number representative of the number of 0 repeat units necessary to achieve the inherent viscosity of It greater than 3.5. 11. The article of claim 7 wherein the fiber is comand y'=1. posed of the polymer represented by the formula:

7. The article of claim 1 wherein said fiber is comwherein n is the number representative for the number of posed of a polymer consisting essentially of recurring repeat units required to achieve the inherent viscosity of para-oriented phenylene rings interlinked through 1 or reater than 3.5.

more of the groups References Cited f i UNITED STATES PATENTS and 3,600,269 8/1971 Daniels et al. 161-170 and combinations thereof. 3,240,660 3/1966 Atwell 161-170 8. The article of claim 7 wherein the fiber is composed 3,243,956 4/ 1966 H m t 1, 161-155 X of a polymer represented by the following formula: 3,303 07 19 7 Shepard 1 70 0 O o 3,388,029 6/1968 Brignac 161170 H H H H 3,411,980 11/1968 Leshin 161227 X C-NH NH'C C OH 3,572,863 3/ 1971 Josephson 161-170 X L\ L, 3,648,452 3/1972 Young l61-170 X wherein n' is a number representative of the number of HAROLD ANSHER Primary Examiner repeat units repuired to achieve an inherent viscosity of greater than 3.5.

9. The article of claim 8 wherein the fiber is a wholly para-oriented polymer. 161227, 239, 247, 255, 256 

